EP2330183A1 - Method of culturing a microorganism - Google Patents

Method of culturing a microorganism Download PDF

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Publication number
EP2330183A1
EP2330183A1 EP10015741A EP10015741A EP2330183A1 EP 2330183 A1 EP2330183 A1 EP 2330183A1 EP 10015741 A EP10015741 A EP 10015741A EP 10015741 A EP10015741 A EP 10015741A EP 2330183 A1 EP2330183 A1 EP 2330183A1
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Prior art keywords
culture
agitation
aeration
amount
fatty acid
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German (de)
English (en)
French (fr)
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Kenichi Higashiyama
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Nissui Corp
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Nippon Suisan Kaisha Ltd
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    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P7/00—Preparation of oxygen-containing organic compounds
    • C12P7/64—Fats; Fatty oils; Ester-type waxes; Higher fatty acids, i.e. having at least seven carbon atoms in an unbroken chain bound to a carboxyl group; Oxidised oils or fats
    • C12P7/6436—Fatty acid esters
    • C12P7/6445—Glycerides
    • C12P7/6472—Glycerides containing polyunsaturated fatty acid [PUFA] residues, i.e. having two or more double bonds in their backbone
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N1/00—Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
    • C12N1/14—Fungi; Culture media therefor
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P7/00—Preparation of oxygen-containing organic compounds
    • C12P7/64—Fats; Fatty oils; Ester-type waxes; Higher fatty acids, i.e. having at least seven carbon atoms in an unbroken chain bound to a carboxyl group; Oxidised oils or fats
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P7/00—Preparation of oxygen-containing organic compounds
    • C12P7/64—Fats; Fatty oils; Ester-type waxes; Higher fatty acids, i.e. having at least seven carbon atoms in an unbroken chain bound to a carboxyl group; Oxidised oils or fats
    • C12P7/6409—Fatty acids
    • C12P7/6427—Polyunsaturated fatty acids [PUFA], i.e. having two or more double bonds in their backbone

Definitions

  • the present invention relates to a method of culturing a microorganism capable of producing at least any one of a highly unsaturated fatty acid and a compound containing a highly unsaturated fatty acid as a constituent fatty acid in a medium containing at least a carbon source and a nitrogen source, using an aeration-agitation culture device capable of adjusting and controlling the agitation power and the aeration amount.
  • KLa volmetric oxygen transfer coefficient
  • KLa as an index in scaled-up culture is based on the idea that the same culture result is obtained irrespective of the type and scale of a culture vessel if the oxygen transfer rate is the same (see, for example, Non-patent Publications 1 and 2).
  • KLa K(P/V) 0.95 (Vs) 0.67 (K: proportionality constant, P: power required for agitation (W), V: liquid amount (m 3 ), Vs: air flow rate (m/sec)) is used (see Non-patent publication 3).
  • KLa can be predicted using the above-described approximate expression proposed by Cooper et al.
  • Cooper et al. obtained a correlation between KLa and operational conditions using a 12-blade vaned disk impeller. Strictly speaking, this correlation cannot be applied to a culture vessel of a type different from that type.
  • An object of the present invention is to provide a culture method capable of scale-up while securing satisfactory productivity of PUFA or a compound containing PUFA as a component without actually calculating KLa (volmetric oxygen transfer coefficient).
  • a method of culturing a microorganism which cultures a microorganism capable of producing at least any one of a highly unsaturated fatty acid or a compound containing a highly unsaturated fatty acid as a constituent fatty acid in a culture medium containing at least a carbon source and a nitrogen source, using an aeration-agitation culture device capable of adjusting and controlling an agitation power and an aeration amount.
  • culture can be performed using a culture medium containing at least a carbon source and a nitrogen source, and the culture medium can be consistently prepared to be uniform due to mechanical agitation. As a result, it is also possible to secure the growth of fungal cells and the reproducibility of productivity of fungal cells.
  • PUFAs a compound containing PUFA as a component
  • the aeration-agitation culture vessel can adjust and control the agitation power and the aeration amount, the dissolved oxygen concentration of culture solution can be adjusted whenever necessary into a range which is suitable for production of PUFAs, for example.
  • a reason to set the required agitation power parameter (P/V) 0.95 [(W/m 3 ) 0.95 ] to 203 or more is that it is intended that agitation is performed at a constant strength or more strongly than when culture is started, preferably more strongly than when culture is started (as shown in Ex.
  • the agitation power per unit liquid amount is 269 (W/m 3 ), i.e., the required agitation power parameter (P/V) 0.95 [(W/m 3 ) 0.95 ] is 203, at the start of culture).
  • the highly unsaturated fatty acid is arachidonic acid.
  • Arachidonic acid accounts for about 10% of fatty acids contained in an important organ, such as blood, liver, or the like (e.g., in the human blood, the ratio of fatty acids in phospholipids is as follows: arachidonic acid 11%, EPA 1%, and DHA 3%).
  • Arachidonic acid is a major component of cell membrane and is involved in adjustment of the fluidity of the membrane to exhibit various functions in the metabolism of the body, and also plays an important role as a direct precursor of prostaglandins.
  • arachidonic acid has attracted attention because of a role of nutrition for suckling infants and as a constituent fatty acid of endogenous-cannabinoid (2-arachidonoyl monoglycerol, anandamide), which exhibits an bility to activate nerves.
  • Linoleic acid taken from linoleic acid-rich food is usually converted to arachidonic acid.
  • arachidonic acid be directly taken as fat or oil (a constituent fatty acid of triglyceride).
  • the present invention may contribute to maintenance or promotion of public health via beverages, therapeutic nutrient foods, feeds, pharmaceuticals, and the like which contain these materials.
  • the fungus producing PUFAs is of the genus Mortierella, subgenus Mortierella.
  • the third feature of the present invention by using a fungus producing PUFAs of the genus Mortierella, subgenus Mortierella, it is possible to produce PUFAs more efficiently, and in addition, the fungi can be easily obtained, as described below and elsewhere herein.
  • the predetermined time after the start of culture is preferably 12 to 24 hours.
  • mechanical agitation having a low level of agitation shearing stress (specifically, agitation power per unit liquid amount is 269 (W/m 3 ) or less) is performed for 12 to 24 hours after the start of culture.
  • agitation power per unit liquid amount is 269 (W/m 3 ) or less
  • a fungus which transforms from a pulp-shaped hypha to a pellet-shaped cell can be caused to efficiently perform such transformation, thereby suppressing a significant increase in the viscosity of subsequent culture solution. Therefore, it is possible to more efficiently produce PUFAs.
  • Examples of a microorganism for use in the present invention which has ability to produce at least any one of PUFA or a compound containing PUFA as a constituent fatty acid (e.g., fat or oil (triglyceride) and /or phospholipid) include the genus Mortierella, the genus Conidiobolus, the genus Pythium, the genus Phytophthora, the genus Penicillium, the genus Cladosporium, the genus Mucor, the genus Fusarium, the genus Aspergillus, the genus Rhodotorula, the genus Entomophthora, the genus Echinosporangium, and the genus Saprolegnia.
  • a microorganism for use in the present invention which has ability to produce at least any one of PUFA or a compound containing PUFA as a constituent fatty acid (e.g., fat or oil (triglyceride)
  • examples of the microorganisms belonging to the genus Mortierella, subgenus Mortierella include Mortierella elongata, Mortierella exigua, Mortierella hygrophila, Mortierella alpina, and the like.
  • fungal strains of Mortierella elongate IFO8570, Mortierella exigua IFO8571, Mortierella hygrophila IFO5941, Mortierella alpina IFO8568, ATCC16266, ATCC32221, ATCC42430, CBS219.35, CBS224.37, CBS250.53, CBS343.66, CBS527.72, CBS529.72, CBS608.70, CBS754.68, and the like can be illustrated.
  • Mortierella elongate SAM0219 (FERM P-8703) (FERM BP-1239), and Mortierella alpina 1S-4, which were isolated from soil by the research group of the present invention, can be used.
  • Mortierella elongata SAM 0219 is internationally deposited under the Budapest Treaty with accession number FERM BP-1239 at International Patent Organism Depositary (IPOD), Japan.
  • a fungal strain for use in the present invention is cultured (main culture) by inoculating a spore or a hypha of the fungal strain, or a seed culture solution obtained by preliminary culture, or a fungal cell recovered from the seed culture onto liquid culture medium.
  • liquid culture medium as the carbon source, any of those which are commonly used, such as glucose, fructose, xylose, saccharose, maltose, soluble starch, molasses, glycerol, mannitol, saccharified starch, and the like, can be used.
  • the present invention is not limited to these.
  • nitrogen source naturally-occurring nitrogen sources (e.g., peptone, yeast extract, malt extract, meat extract, casamino acid, corn steep liquor, soybean protein, defatted soybean, cottonseed meal, etc.), organic nitrogen sources (e.g., urea, etc.), and inorganic nitrogen sources (e.g., sodium nitrate, ammonium nitrate, ammonium sulfate, etc.) can be used.
  • organic nitrogen sources e.g., urea, etc.
  • inorganic nitrogen sources e.g., sodium nitrate, ammonium nitrate, ammonium sulfate, etc.
  • specific examples of a nitrogen source obtained from soybean include soybean, defatted soybean, soybean flake, edible soybean protein, soybean meal, bean curd, soy flour, and the like.
  • defatted soybean which is denatured by heat, more preferably defatted soybean which is treated by heating at about 70 to 90°C, followed by removal of ethanol soluble components, can be used singly or multiply, or in combination with the above-described nitrogen sources.
  • metal ions e.g., iron, copper, zinc, manganese, nickel, cobalt, etc.
  • vitamins, and the like can be optionally used as a small amount of nutrient source in addition to phosphate ion, potassium ion, sodium ion, magnesium ion, and calcium ion.
  • These culture medium ingredients are not particularly limited if they have a concentration which does not inhibit the growth of a microorganism.
  • the total amount of added carbon source(s) is generally 0.1 to 40% by weight, preferably 1 to 25% by weight, and the total amount of added nitrogen source(s) is 2 to 15% by weight, preferably 2 to 10% by weight.
  • the starting amount of added carbon source(s) is 1 to 5% by weight, and the starting nitrogen source concentration is 3 to 8% by weight, and a carbon source(s) and a nitrogen source(s) are added at some point(s) during culture (more preferably, only a carbon source(s) is added).
  • hydro carbon such as hexadecane or octadecane
  • fatty acid such as oleic acid or linoleic acid, or a salt or a fatty acid ester thereof (e.g., ethyl ester, glycerin fatty acid ester, sorbitan fatty acid ester); or fats and oils, such as olive oil, soybean oil, rape oil, cottonseed oil, or coconut oil, can be used as precursors of unsaturated fatty acid, singly or in combination.
  • the added amount of these substrates is 0.001 to 10% with respect to culture medium, preferably 0.5 to 10%. These substrates may serve as the only carbon source for culture.
  • culture temperature varies depending on microorganisms used.
  • the culture temperature is 5 to 40°C, preferably 20 to 30°C.
  • microorganisms can be cultured and grown at 20 to 30°C, followed by culture at 5 to 20°C to produce unsaturated fatty acid.
  • the proportion of highly unsaturated fatty acid in the produced fatty acid can be increased.
  • Aeration-agitation culture, shaking culture, solid culture, or still liquid culture is performed in seed culture, while aeration-agitation culture is performed in main culture.
  • the pH of culture medium is adjusted to 5 to 7, preferably 5.5 to 6.5.
  • the period of the main culture is usually 2 to 30 days, preferably 5 to 20 days, and more preferably 5 to 15 days.
  • microorganisms belonging to the genus Mortierella, subgenus Mortierella can produce a fat or an oil (triglyceride) having arachidonic acid as a major constituent fatty acid.
  • the present inventors have obtained a microorganism capable of producing fat or oil (triglyceride) having dihomo- ⁇ -linoleic acid as a major constituent fatty acid ( JP H05-91887 A ) and a microorganism capable of producing a fat or an oil (triglyceride) having ⁇ 9 highly unsaturated fatty acid as a major constituent fatty acid ( JP H05-91888 A ) by introducing mutation into the above-described fungal strain.
  • the present inventors have also obtained a microorganism resistant to a high-concentration carbon source ( WO98/39468 ). These microorganisms belong to the genus Mortierella, subgenus Mortierella, and the productivity thereof can be improved by culture using the culture method of the present invention.
  • the culture is conducted while performing relatively weak mechanical agitation (agitation power per unit liquid amount: 269 (W/m 3 ) or less), and aeration.
  • relatively weak mechanical agitation agitation power per unit liquid amount: 269 (W/m 3 ) or less
  • the amount of aeration is not particularly limited.
  • the microorganisms may change their forms from a pulp-shaped hypha to a pellet-shaped fungal cell (also called as a spherical hypha) when going from the vegetative phase to the productive phase.
  • the pellet-shaped fungal cell refers to one fungal form of actinomycetes and filamentous fungi when cultured in liquid culture medium, specifically indicating a spherical or spindle-shaped hypha aggregation having an average diameter of 0.2 to several millimeters.
  • the pulp-shaped hypha refers to a typical fungal form of actinomycetes and filamentous fungi when cultured in liquid culture medium, specifically indicating that linearly or radially elongated hyphae distributed.
  • the transformation from the pulp-shaped hypha to the pellet-shaped fungal cell is closely related with the productivity of PUFAs.
  • an optimum culture medium composition is studied or the partial pressure of oxygen in aeration gas is adjusted.
  • agitation having low agitation shearing stress is performed for a predetermined time from the start of culture, thereby promoting transformation of fungal cells to the pellet-shape.
  • the aeration-agitation device is equipped with a dissolved oxygen concentration detecting sensor to monitor the dissolved oxygen concentration of culture solution.
  • the dissolved oxygen concentration (DO) of culture medium starts to decrease with the growth of fungal cells.
  • the agitation power and the amount of aeration are increased immediately before the DO value reaches the lower limit (about 50%) above which the productivity of PUFAs is not influenced, thereby adjusting and maintaining the DO value.
  • the adjustment and control it is considered that either or both of the maximum aeration amount and the maximum power required for agitation are increased.
  • culture is performed for 5 to 15 days while adding glucose culture medium whenever necessary during culture.
  • the fungal cells are recovered and dried, followed by hexane extraction of the dried fungal cells to obtain at least any one of PUFA and a compound (e.g., triglyceride, phospholipid, etc.) containing PUFA as a constituent fatty acid.
  • a compound e.g., triglyceride, phospholipid, etc.
  • Effective power was measured using a power meter (clamp-on power meter manufactured by Hioki E. E. Corporation) which was provided on a first-order side (power source side) of an inverter.
  • a culture medium containing 1% yeast extract, 2% glucose, 0.1% soybean oil, and having a pH of 6.3 was prepared in a 50-L capacity aeration-agitation culture vessel.
  • the culture medium was inoculated with the seed culture (first stage) solution, and seed culture (second state) was started where the agitation rotational speed was 200 rpm, the temperature was 28°C, and the vessel pressure was 150 kPa, and was performed for 2 days.
  • a culture medium for main culture was prepared in a 10-kL capacity aeration-agitation vessel (the inner diameter of the culture vessel is 1.8 m).
  • the culture medium was prepared in the following manner. Initially, 4500 L of a culture medium (culture medium A: soybean flour 336 kg; KH 2 PO 4 16.8 kg; MgCl 2 ⁇ 6H 2 O 2.8 kg; CaCl 2 ⁇ 2H 2 O 2.8 kg; soybean oil 5.6 kg) was prepared to pH 4.5, and was sterilized in the main culture vessel at 121°C for 20 minutes.
  • culture medium A soybean flour 336 kg; KH 2 PO 4 16.8 kg; MgCl 2 ⁇ 6H 2 O 2.8 kg; CaCl 2 ⁇ 2H 2 O 2.8 kg; soybean oil 5.6 kg
  • culture medium B water-containing glucose 112 kg
  • culture medium C the culture medium after addition
  • Sterilized aqueous sodium hydroxide solution was sterilely added to the culture medium C and was adjusted to pH 6.1, and thereafter, the seed culture solution (second stage) having a volmetric capacity of 28 L was inoculated to the culture medium C by sterile manipulation, resulting in a total of 5600 L (starting culture liquid amount) (the culture vessel has a volmetric capacity of 10 kL).
  • Values of the parameters at the high aeration-agitation level were calculated as follows. P / V 0.95 : 2169 W / m 3 0.95 Vs 0.67 : ⁇ 0.130 m / sec 0.67
  • KLA P / V 0.95 ⁇ Vs 0.67 : 282 W / m 3 0.95. ⁇ m / sec 0.67
  • the main culture was performed for 306 hours while adding culture medium at some point(s) during culture as described below.
  • the culture liquid amount was 7750 L due to the addition (increase) and the evaporation (decrease) of culture medium.
  • the wet fungal cells were recovered using a continuous hydroextractor, followed by drying with hot air (hot air temperature: 120°C) using a shaking fluid bed dryer to a water content of 2 % by weight (wt%).
  • the dried fungal cell was cooled to 40°C in a fluid bed by supply of room air, and was then transported to a loading place using a pneumatic conveyor.
  • the resultant dried fungal cell was loaded along with nitrogen gas into an aluminum container bag (pouch) having a volmetric capacity of about 1 m 3 , and the mouth of the bag was sealed by heat.
  • the bag was preserved at 10°C or less in a refrigerator.
  • the dried fungal cell removed from the container bag was subjected to hexane extraction.
  • the hexane solution was filtered to remove solid components thereof. Thereafter, the resultant solution was heated under reduced pressure to remove hexane, thereby obtaining crude oil having arachidonic acid as a constituent fatty acid.
  • Seed culture was performed and a culture medium for main culture was prepared using a method similar to that of Example 3.
  • the main culture was performed under the same conditions as those of Example 3, except that conditions for agitation at the start of culture were set to be various values as shown in a table below.
  • Seed culture was performed and a culture medium for main culture was prepared using a method similar to that of Example 3.
  • the main culture was performed under the same conditions as those of Example 3, except that conditions for aeration at the start of culture were set to be various values as shown in a table below.
  • conditions for aeration at the start of culture were set to be various values as shown in a table below.
  • a method of stopping aeration intermittently was adopted in order to suppress bubbling.
  • An air flow rate Vs in Example 5 is an air flow rate when aeration is being performed, but not an average accumulated amount of aeration obtained taking the intermittent aeration in account.
  • the lower limit of the DO value above which the productivity of arachidonic acid is not influenced is a DO concentration (critical DO concentration) below which a lineal relationship between a decrease in DO due to the stop of aeration and an elapsed time is lost.
  • the critical DO concentration was previously obtained using a dynamic measuring method ("Hakkokogaku no Kiso (Principles of Fermentation Technology)", 1988, Gakkai Shuppan Senta, translated by Ayaaki Ishizaki), where culture was performed under the same conditions.
  • P/V power required for agitation
  • the main culture was performed for 306 hours while adding glucose having the same concentration as that of Example 3 at some point(s) during the culture. As a result, 20.0 g/L of produced arachidonic acid (corrected value) was obtained.
  • Mortierella alpina strain CBS754.68 was used as an arachidonic acid producing fungus.
  • the preserved fungal strain was used to perform seed culture and a culture medium for main culture was prepared using a method similar to that of Example 3.
  • Values of the parameters at the time of start of culture were calculated as follows.
  • the main culture was performed for 288 hours while adding glucose at some point(s) during the culture as in Example 3.
  • Mortierella alpina strain SAM1860 was used as a dihomo- ⁇ -linoleic acid producing fungus.
  • the preserved fungal strain was inoculated into a culture medium containing 1% yeast extract and 2% glucose and having a pH of 6.3, which was prepared in a flask, followed by seed culture (first stage) at 100 rpm at 28°C for 3 days.
  • a culture medium containing 1% yeast extract, 2%, glucose, and 0.1% soybean oil and having a pH of 6.3 was prepared in a 50-L capacity aeration-agitation culture vessel, and was inoculated with the culture solution previously obtained by the seed culture (first stage), followed by seed culture (second stage) for 2 days where the agitation rotational speed was 200rpm, the temperature was 28°C, and the vessel internal pressure was 150 kPa.
  • a culture medium containing 4% defatted soybean flour, 1.8% glucose, 0.3% KH 2 PO 4 , 0.1% Na 2 SO 4 , 0.05% MgCl 2 ⁇ 6H 2 O, 0.05% CaCl 2 ⁇ 2H 2 O, and 0.1% soybean oil and having a pH of 6.1 was inoculated with 0.5% of the seed culture solution (second stage).
  • Main culture was started with 4000 L (liquid amount) of the culture medium.
  • Values of the parameters at the time of start of culture were calculated as follows. P / V 0.95 : 25 W / m 3 0.95 Vs 0.67 : 0.0313 m / sec 0.67
  • KLA P / V 0.95 ⁇ Vs 0.67 : 0.782 W / m 3 0.95. ⁇ m / sec 0.67
  • the main culture was performed for 160 hours while adding glucose at some point(s) during the culture.
  • the concentration of produced dihomo- ⁇ -linoleic acid was 7.0 g/L at the end of culture.
  • Mortierella alpina strain SAM2086 was used as a mead acid producing fungus.
  • the preserved fungal strain was inoculated into a culture medium containing 1% yeast extract and 2% glucose and having a pH of 6.3, which was prepared in a flask, followed by seed culture (first stage) at 100 rpm at 28°C for 3 days.
  • a culture medium containing 1% yeast extract, 2% glucose, and 0.1% olive oil and having a pH of 6.3 was prepared in a 50-L capacity aeration-agitation culture vessel, and was inoculated with the culture solution previously obtained by the seed culture (first stage), followed by seed culture (second stage) for 2 days where the agitation rotational speed was 200rpm, the temperature was 28°C, and the vessel internal pressure was 150 kPa.
  • a culture medium containing 4% defatted soybean flour, 1.8% glucose, 0.3% KH 2 PO 4 , 0.1% Na 2 SO 4 , 0.05% MgCl 2 ⁇ 6H 2 O, 0.05% CaCl 2 ⁇ 2H 2 O, and 0.1% olive oil, and having a pH of 6.1 was inoculated with 0.5% of the seed culture solution (second stage).
  • Main culture was started with 4000 L (liquid amount) of the culture medium.
  • Values of the parameters at the time of start of culture were calculated as follows. P / V 0.95 : 25 W / m 3 0.95 Vs 0.67 : 0.0313 m / sec 0.67
  • KLA P / V 0.95 ⁇ Vs 0.67 : 0.782 W / m 3 0.95. ⁇ m / sec 0.67
  • the culture was started under these conditions.
  • Values of the parameters at the high aeration-agitation level were calculated as follows.
  • the main culture was performed for 376 hours while adding glucose at some point(s) during the culture.
  • the concentration of produced mead acid was 6.0 g/L at the end of culture.
  • At least any one of arachidonic acid which particularly plays an important role as a nutrient for suckling infants, or a compound (e.g., fats, oils, etc.) containing arachidonic acid as a constituent fatty acid, can be efficiently and stably produced. Therefore, the present invention is useful for production of beverages, therapeutic nutrient foods, feeds, pharmaceuticals, and the like which contain these materials.
  • the invention furthermore comprises the following items:

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EP10015741A 2004-09-06 2005-09-05 Method of culturing a microorganism Withdrawn EP2330183A1 (en)

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JP2004258151A JP4624040B2 (ja) 2004-09-06 2004-09-06 菌体培養方法
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US20080064076A1 (en) * 2006-09-11 2008-03-13 Saucedo Victor M Dissolved Oxygen Profile to Increase Fermentation Productivity and Economics
US8889907B2 (en) 2008-03-14 2014-11-18 Mitsubishi Rayon Co., Ltd. Process for production of amide compounds
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